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Envelope type reactor thermal-transferring method in methanol synthesizing process

A shell-and-tube reactor and methanol synthesis technology, which is applied to chemical instruments and methods, preparation of organic compounds, lighting and heating equipment, etc., can solve the problems of not being able to move out of the methanol synthesis tower in a sufficient and timely manner, so as to increase water volume and meet Effect of high load requirements

Inactive Publication Date: 2008-12-31
刘宏建 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In order to overcome the defect in the above-mentioned prior art that the amount of water entering the shell side of the methanol synthesis tower is small and the heat of reaction released during overloading cannot be removed from the methanol synthesis tower in a timely manner, the present invention provides a shell-and-tube reaction for the methanol synthesis process The heat removal method of the device, using the "shell-and-tube type methanol synthesis tower shell side hydrodynamic circulation device" previously applied by the applicant to achieve faster and more timely removal of more water by increasing the amount of water entering the methanol synthesis tower shell side Reaction heat, make full use of the efficiency of methanol synthesis reaction tower, save energy, reduce cost, increase output value and output

Method used

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  • Envelope type reactor thermal-transferring method in methanol synthesizing process
  • Envelope type reactor thermal-transferring method in methanol synthesizing process
  • Envelope type reactor thermal-transferring method in methanol synthesizing process

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Embodiment approach 1

[0016] As shown in Figure 2: the shell-and-tube reactor heat transfer method of the methanol synthesis process of the present invention adopts the shell-and-tube methanol synthesis reactor, and the methanol synthesis reaction uses the gas containing carbon monoxide, carbon dioxide and hydrogen as raw materials, which enters after compression The shell side of the intermediate heat exchanger (1), after being heated to the reaction temperature, enters the tube side of the methanol synthesis tower (2), and under the action of a catalyst, the synthesis reaction gas undergoes methanol synthesis reaction; part of the synthesis reaction gas temperature rises , the gas out of the synthesis tower enters the tube side of the intermediate heat exchanger (1), and after being cooled, it enters the methanol condenser (4), and after the methanol is condensed, it enters the methanol separator (5). After the methanol is separated, the unreacted The gas returns to the inlet of the circulating co...

Embodiment approach 2

[0020] As shown in Figure 3: the shell-and-tube reactor heat removal method of methanol synthesis process of the present invention, it also can adopt another kind of water supply circulation system, valve (9) is installed on the downcomer of former steam drum, and valve also can be automatic valve , the valve (9) pipeline on the downcomer is connected in parallel with the water pump (6) pipeline, that is, the two ends of the valve (9) are respectively connected to the circulating water pump (6) through the input pipeline and output pipeline of the water pump (6), An input valve (7) and an output valve (8) are respectively installed on the input pipeline and the output pipeline; the water pump (6) can also be designed as two sets, and when the water pump (6) has an empty pump failure, the other water pump can automatically Work, guarantee that the water supply circulation system is normal; Water pump (6) also can be designed to automatic control, break down when water pump works...

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Abstract

A shell-and-tube reactor heat transfer method for a methanol synthesis technology adopts a shell-and-tube methanol synthesis reactor and comprises the following steps: (1), a majority of the heat released through the reaction of the methanol synthesis tower is transferred to the boiling water in the shell side; by adding a set of water supply circulation system into the system of the original methanol synthesis circulated based on the water density difference, the methanol synthesis reaction heat is removed from the system and the water-containing part is vaporized to take away the heat generated in the reaction; (2), the water inside a steam drum (3) in the water supply circulation system enters a circulating pump through a vertical pipe and an input valve (7); the circulating pump is pressurized and enters the shell side of the methanol synthesis tower (2) through an output valve (8) so as to greatly increase the water amount of the shell side of the synthesis tower; when the water inside the shell side of the synthesis tower is heated and vaporized into small bubbles; the small bubbles can directly enter into the steam drum (3) through a rising pipe so as to take away more heat to meet high-load requirements.

Description

technical field [0001] The invention belongs to the technical field of methanol synthesis, and in particular relates to a heat transfer method for a shell-and-tube reactor in a methanol synthesis process. Background technique [0002] At present, in methanol production plants, most of them use shell-and-tube methanol synthesis reactors. The methanol synthesis reaction uses gas containing carbon monoxide, carbon dioxide and hydrogen as raw materials, which enters the shell side of the intermediate heat exchanger (1) after being compressed, and enters the tube side of the methanol synthesis tower (2) after being heated to the reaction temperature. Next, the synthetic reaction gas is used for the methanol synthesis reaction. Most of the heat released by the reaction is transferred to the boiling water on the shell side, and the heat generated by the reaction is taken away by the partial vaporization of the water. Part of the temperature of the synthesis reaction gas rises, an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C31/04C07C29/152F25J3/00
Inventor 刘宏建高恒
Owner 刘宏建
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